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WO2005089727A1 - Procede pour produire des particules de type coeur-ecorce et des microcapsules au moyen de matrices microporeuses, particules de type coeur-ecorce et microcapsules, et leur utilisation - Google Patents

Procede pour produire des particules de type coeur-ecorce et des microcapsules au moyen de matrices microporeuses, particules de type coeur-ecorce et microcapsules, et leur utilisation Download PDF

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Publication number
WO2005089727A1
WO2005089727A1 PCT/EP2005/002810 EP2005002810W WO2005089727A1 WO 2005089727 A1 WO2005089727 A1 WO 2005089727A1 EP 2005002810 W EP2005002810 W EP 2005002810W WO 2005089727 A1 WO2005089727 A1 WO 2005089727A1
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WIPO (PCT)
Prior art keywords
porous
particles
microcapsules
templates
template
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Ceased
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PCT/EP2005/002810
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German (de)
English (en)
Inventor
Lars DÄHNE
Barbara Baude
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Capsulution Nanoscience AG
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Capsulution Nanoscience AG
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Priority to EP05716128A priority Critical patent/EP1729745B1/fr
Priority to CA002559477A priority patent/CA2559477A1/en
Priority to JP2007503286A priority patent/JP2007529303A/ja
Priority to US10/593,353 priority patent/US7939103B2/en
Publication of WO2005089727A1 publication Critical patent/WO2005089727A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5073—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals having two or more different coatings optionally including drug-containing subcoatings
    • A61K9/5078—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals having two or more different coatings optionally including drug-containing subcoatings with drug-free core
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5073—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals having two or more different coatings optionally including drug-containing subcoatings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
    • Y10T428/2991—Coated

Definitions

  • Microcapsules made of alternately adsorbed polyelectrolyte layers are known, for example, from [1] and are described in DE 198 12 083 AI, DE 199 07 552 AI, EP 0 972 563 AI, WO 99/47252 and US 6,479,146, the contents of which are disclosed is hereby fully incorporated.
  • Capsule systems of this type have a high potential for use as microreactors, drug delivery systems, etc. due to their adjustable semipermeability. Prerequisite is the filling with appropriate active substances, enzymes, polymers or catalysts.
  • Porous CaCO 3 templates [9] This approach uses porous CaCO 3 templates.
  • the templates are suspended in solutions of alternately charged polyelectrolytes.
  • the outer and inner surfaces of the porous templates are coated with polyelectrolytes.
  • microcapsules remain with an inner framework made of polyelectrolytes, which is surrounded by an unclosed polyelectrolyte shell. Macromolecules can then be attached to the inner framework of the microcapsules. A closed capsule shell cannot be produced with this method, since the pores of the CaCO 3 template are relatively large.
  • the object of the present invention is therefore to provide a method for encapsulating materials or active ingredients, in which the active ingredients to be encapsulated can be easily and in high concentration enriched inside the capsules.
  • this object is achieved by a method for producing CS particles and / or microcapsules with the following steps: - at least one active ingredient to be encapsulated is adsorbed in porous templates; a capsule shell is formed around the porous template by applying alternately charged polyelectrolyte and / or nanoparticle layers.
  • CS particles that still contain the porous template as the core with the adsorbed active ingredient.
  • the porous template can subsequently be detached from the CS particles, producing microcapsules that are filled with the active ingredient.
  • at least one primer layer can be applied to the porous template. Possibly. additional layers of polyelectrolytes and / or nanoparticles are applied to the primer layer before the actual capsule shell is formed.
  • the capsule shells are alternated by sequential adsorption charged polyelectrolytes produced (so-called LbL process).
  • LbL process sequential adsorption charged polyelectrolytes produced
  • porous templates are understood to mean those particles which have a large number of pores or internal cavities.
  • core-shell (CS) particles are obtained, which are referred to as CS particles.
  • CS particles core-shell particles.
  • an inner primer layer which in the simplest case is filled with the external solvent or with a solution or suspension of the enclosed active substance.
  • the CS particles or microcapsules are filled with the active ingredient, i.e.
  • the active ingredient remains in the CS particles or microcapsules, since the capsule shell acts as a diffusion barrier with respect to the active ingredient.
  • Colloidal particles that are used to fill the porous particles or to build up the LbL shell and are therefore generally smaller than 100 nm are referred to as nanoparticles.
  • the invention described here offers a new, simple and general method for encapsulating materials even in high concentration in CS particles and microcapsules (layer by layer polyelectrolyte capsules).
  • LbL CS particles and microcapsules filled with active ingredients are produced with the help of porous templates.
  • the porous templates are filled with one or more active ingredients before the LbL coating. If the active ingredient is insufficiently adsorbed in the pores, special auxiliaries (mediators) or pH changes can be used to improve the filling.
  • the filled templates are coated with a special primer that does not penetrate the pores, but seals them for subsequent coatings.
  • the capsule shell or wall is then built up alternating adsorption of polycations and polyanions, which creates a filled CS particle.
  • the porous templates can be removed with solvents.
  • silica particles (SiO) in particular, this can be carried out under mild conditions above pH 4, for example to protect biological active substances
  • the templates used are porous microparticles, the size of which is preferably less than 100 ⁇ m.
  • the microparticles have pores with, for example, a pore size of 0.3 nm to 100 nm, preferably 1 nm to 30 nm and particularly preferably 6 nm to 10 nm.
  • the lower limit of the pore size can be between 1 nm and 6 nm, for example at 2 nm or 4 nm
  • the upper limit of the pore size between 10 nm and 40 nm, for example at 15 nm or 30 nm.
  • the pore size should be so large that the active ingredients to be encapsulated penetrate into the pores and can be deposited in the pores, i.e. adsorb particularly inside the pores.
  • Porous templates with a large inner surface are therefore preferred, the inner surface being formed by the inner walls of the pores.
  • the inner 4 that is actually available for the adsorption of the active substances should be
  • the effective inner surface is understood here to mean that part of the surface which is actually available for the adsorption of an active substance of a certain size. Since the templates often have pores with different widths, large-molecular active substances can only penetrate into correspondingly large pores, while smaller pores are also available for smaller molecules. The pore size can therefore also be described via the size of the nanoparticles or molecules or their molecular weight, which can still penetrate into the pores.
  • the lower limit of the molecular weight is preferably 100 g / mol.
  • the upper limit corresponds to a molecular weight of approximately 5 ⁇ 10 6 g / mol.
  • the shape of the molecule to be penetrated also plays an important role.
  • the surface of the pore cavities is preferably coated with the LbL technology by means of several layers of alternately charged polyelectrolytes and / or nanoparticles, ie polyelectrolyte and / or nanoparticle layers are formed on the "inner" surface of the porous template.
  • the size of the nanoparticles or the molecular weight of the polyelectrolytes is adapted accordingly to the pore size.
  • a filigree negative impression of the original pore structure consisting of insoluble complexes of polyelectrolyte complexes and / or polyelectrolyte / nanoparticle complexes (inner framework) is obtained, which mechanically stabilizes the capsules and greatly increases their inner surface.
  • the active ingredient to be encapsulated in this case is the material of the inner framework.
  • a further active ingredient can be embedded in and / or attached to the inner framework (for example by precipitation and / or adsorption), which is then bound, for example, to the inner framework.
  • the advantage of an inner framework is a significant increase in the inner surface of the microcapsules.
  • CS particles with a diameter smaller than 100 ⁇ m; a porous core in which at least one active ingredient is adsorbed; and a capsule shell made of several layers of alternately charged polyelectrolyte and / or nanoparticle layers.
  • the porous core is the porous template described. Possibly. can be arranged between the porous core and the capsule shell, a primer layer which surrounds the core and contributes to improving the structure of the capsule shell.
  • microcapsules with a diameter smaller than 100 ⁇ m; a capsule shell made of several layers of alternately charged polyelectrolyte and / or nanoparticle layers; - a primer layer on the inside of the capsule shell; and - at least one active substance which is enclosed inside the microcapsules.
  • the porous template or core has been removed.
  • microtemplates with the following steps: at least one porous template is provided; the surface of the pore cavities of the porous template is coated with several layers of alternately charged polyelectrolytes and / or nanoparticles; and the porous template is dissolved, leaving a microtemplate consisting of the polyelectrolyte and / or nanoparticle layers.
  • the polyelectrolyte and / or nanoparticle layers can optionally be crosslinked before or after the template is dissolved (for example covalently) in order to increase the stability of the microtemplate.
  • a filigree framework that largely corresponds to a negative impression of the inner pore structure of the template and here represents the micro template.
  • polyelectrolyte and / or nanoparticle layers are formed on the outside of the template, which remain even after the template has been dissolved.
  • the shell formed in this way is only partially or largely completely constructed.
  • the microtemplate formed can now be the starting point for the production of further microparticles, for example active substances can be attached to the framework.
  • the microtemplates are characterized by a relatively large surface area with a small volume and therefore offer many binding sites for active substances to be added.
  • no capsule shell with an optional primer layer is formed in the microtemplates after the template has been filled with polyelectrolyte and / or nanoparticle layers.
  • the microtemplate and the microcapsules with an inner framework can be produced using the same materials and under the same conditions.
  • the size of the microtemplate corresponds to the size of the template used and is therefore in the range specified above.
  • the CS particles and / or microcapsules produced and filled with the active ingredient can be used advantageously in many areas, for example for encapsulating substances in the areas of diagnostics and sensors; and / or - for the selective accumulation of substances from solutions for applications in water purification, diagnostics, nuclear chemistry, etc .; and / or - for the inclusion of catalytically active substances, in particular metals and / or metal oxides and / or enzymes for the catalysis of chemical and biochemical reactions; and / or - for encapsulating nanoparticles, in particular for producing fluorescent or magnetic microcapsules, for diagnostic or medical applications; and / or - for encapsulation and release of active ingredients in the pharmaceutical and cosmetic industry; and / or - for separation purposes, for example in chromatography; and / or for applications in the food industry and agriculture and forestry.
  • FIG. 1 shows individual process steps of the process according to the invention and the CS particles or microcapsules obtained in the process
  • FIG. 2 a) and b) CS particles and c) microcapsules with an encapsulated positive polymer;
  • Figure 3 a) CS particles and b) microcapsules with an encapsulated negative polymer;
  • Figure 4 a) CS particles and b) microcapsules with an encapsulated zwitterionic protein;
  • Figure 5 a and b) CS particles and c and d) microcapsules with several encapsulated active ingredients;
  • FIG. 6 a) capsules filled with nanoparticles b) superparamagnetism in capsules filled with nanoparticles;
  • For 7 a) and b) CS particles and c) and d) microcapsules filled with a PAH-Rho / PSS complex framework; and
  • FIG. 8 process steps for the production of microtemplates.
  • FIG. 1A shows the filling with an active ingredient that is permanently immobilized inside at a later point in time or is released in a metered manner if the wall permeability is appropriate.
  • FIG. 1B shows the formation of a microcapsule with an inner framework.
  • the active substance can be any material that 1. can be accumulated inside porous templates and 2. can be retained with a LbL shell for a certain period of time.
  • the active ingredients can be molecular, aggregated, complex or colloidal.
  • the active ingredients to be encapsulated are
  • Polymers and / or proteins and or organic molecules with molecular weights over 100 g / mol and / or nanoparticles can be enzymes and / or catalysts and / or dyes and / or pharmaceutical or cosmetic active ingredients and or crop protection agents.
  • the active ingredients to be encapsulated can have a different affinity or
  • Affinity can be exploited when loading the template with several active ingredients.
  • Porous templates 2 are, in particular, colloidal inorganic and organic particles in the size range between 100 nm and 100 ⁇ m suitable for LbL capsules between 500 nm and 15 ⁇ m or 30 ⁇ m. The smallest possible distribution of the pore size of this template 2 is preferred, ie the pores should preferably have largely the same pore size.
  • porous colloidal silica particles and / or zeolites and / or organic polymer particles are suitable as templates, since these particles can be produced with a sufficiently narrow distribution of the pore size.
  • Porous zeolite particles have a pore size of in particular 0.3 nm to 10 nm.
  • step A The filling of the porous template 2 with one or more active substances 4 can be mediated by attractive interaction, for example by adsorption of the active substances and template 2 present in a solution (for example an aqueous medium) via electrostatic and / or H-bridge bonds and / or specific interactions and / or van der Waals interactions take place.
  • Organic or inorganic materials can serve as active ingredients for which
  • Layer by layer films are impermeable or not very permeable. These materials can be in solution, in the form of a solid framework or in colloidal form as nanoparticles.
  • Electrostatic are particularly suitable for adsorption in the porous templates
  • Variants in question 1. By shifting the pH value, the active substances themselves or the surface of the template are reloaded. This creates an attractive interaction. In particular, biopolymers with an isoelectric point can be adsorbed relatively easily in the templates. 2.
  • the adsorption of the active substances is mediated by means of suitable auxiliary substances (mediators).
  • the auxiliary substances can, for example, reload the surface of the pores or also enable specific interactions between the active substances (eg proteins, peptides, further active substances) and the pore surface.
  • the use of auxiliaries in particular allows one Transfer of surfaces with subsequent adsorption of the active substances charged in the same direction.
  • Auxiliaries can also be macromolecules 14 (FIG.
  • active ingredients can be adsorbed one after the other or simultaneously.
  • pore sizes are used that are matched to the size of the molecules to be filled.
  • molecules between 0.1 and 5000 kDa 100 g mol - 5,000,000 g / mol
  • the active ingredient with the higher binding constant is filled in the deficit, ie its concentration is chosen so that this active ingredient does not occupy all available binding sites.
  • the incompletely filled particles are then filled with the second active ingredient in a solution by adsorption. in the As a result, the templates 4 are largely filled with the active ingredient (s) 4.
  • Primer (step B) A primer layer 6 made of, for example, a polyelectrolyte or of nanoparticles is optionally applied to the now filled template 5.
  • the primer material must be selected and adjusted so that 1. it does not penetrate the filled pores itself, 2. prevents the materials used in the subsequent construction of the LbL capsule shell from penetrating into the interior the size of the pores are adjusted.
  • the primer material 6 typically differs from the materials of the casing to be subsequently applied. Possibly. it can also be a polyelectrolyte, which, however, has a higher molecular weight and / or a more branched structure and / or better crosslinking than the LbL capsule shell materials.
  • an extra networking step e.g. be carried out via glutaraldehyde in the case of amino-functionalized polyelectrolytes.
  • alternating layers 8 of cationically and anionically charged substances are applied to this primer layer 6 until the desired semi- or impermeability of the LbL capsule wall 9 for the enclosed substance is reached.
  • the permeability of the LbL capsule can be specifically adjusted for the respective encapsulated material by the number of layers, the selection of the material, by post-treatment by annealing, or by the implementation of further substances in the capsule wall [8] .
  • CS particles 10 with a filled porous core.
  • Suitable substances for forming the capsule wall and a suitable process sequence can be found in the already mentioned documents DE 198 12 083 AI, DE 199 07 552 AI, EP 0 972 563 AI, WO 99/47252 and US 6,479,146.
  • step D A subsequent optional dissolution of the cores (template) from the CS particles 10 takes place with a suitable solvent.
  • solvents can be organic liquids such as polystyrene tetrahydrofuran, or acidic or basic aqueous solutions such as melamine formaldehyde resins HC1 [6] .
  • silica particles can be easily dissolved with 1mol / 1 HF, since the resulting products (SiF 6 2 ) easily diffuse out through the capsule membrane without damaging the capsule wall. ⁇ 3 1 molar HF is not without problems for many materials.
  • a fluoride salt with a concentration of 1-5 mol / 1 is adjusted to a desired pH of 3-6 with a buffer solution 1-5 mol / 1.
  • porous silicate plates dissolve without residues if the reaction time is sufficient.
  • the hexafluorosilicate anions easily diffuse out of the capsules through thick LbL layers.
  • the preferred pH range is from 3 or 3.5 (lower limit) to 6 or 6.5.
  • the described method for dissolving the template can be used regardless of whether it is porous or non-porous microparticles and is particularly suitable for dissolving porous and non-porous silica and zeolite particles.
  • this method is basically suitable for dissolving such materials, these materials being dissolved in the pH range from 3.5 to 6 by fluoride salts in the presence of a buffer solution, in particular an acetate / acetic acid buffer.
  • This solution method is particularly suitable for acid-sensitive materials that either form the capsule wall or are enclosed inside. This affects many biopolymers such as proteins, enzymes, DNA, but also acid-sensitive polymers or nanoparticles, such as magnetite or quantum dots (fluorescent nanoparticles).
  • step E optionally release of the active ingredient
  • microcapsules 12 filled with an active substance FOG. 1A
  • microcapsules 13 provided with an inner framework 16 are present.
  • the active substances remain permanently immobilized inside the microcapsules or are released within a defined period of time.
  • PAH-Rho poly (allylamine hydrochloride)
  • the CS particles were incubated with 100 mL of a solution of 2 mol / l sodium fluoride in 1 mol / l acetate buffer (pH 4). After 3 hours, the templates (cores) have completely dissolved and the capsules filled with PAH remain (FIG. 2c). After several wash cycles with water, one was inside the capsules Concentration of 6.3 g / 1 PAH-Rho determined, which did not change after storage for several weeks.
  • FIG. 2 shows CS particles and capsules produced with a positively charged polymer inside; a) confocal image of CS particles filled with PAH-Rho, primed with Chitosan-Flu and coated with 7 layers of PAH / PSS (rhodamine channel PMT2 600 V, image size 80 ⁇ m x 80 ⁇ m); b) confocal image of the CS particles (fluorescein channel PMT1 750 V, image size 80 ⁇ m x 80 ⁇ m); c) Confocal image of Chitosan (PSS / PAH) 3 PSS capsules filled with PAH-Rho after the SiO 2 template has been removed (rhodamine channel PMT2 600V, image size 80 ⁇ m x 80 ⁇ m).
  • Negatively charged polymer 10 mg of spherical, porous silicate plate with a diameter of 10 ⁇ m and a pore size of 7 nm are suspended in 100 ⁇ L water (pH 6.5). The templates are then incubated in a 0.1 mol / l solution of FeCl 3 . After three washing cycles with water, 500 ⁇ L of a solution of 1 g / 1 rhodamine-labeled polystyrene sulfonate (PSS, MW 130,000 g / mol Capsulution Nanoscience AG) were added and incubated for 12 h. The anionically charged PSS-Rho has adsorbed on the surface of the pores via Fe 3+ .
  • PSS 1 g / 1 rhodamine-labeled polystyrene sulfonate
  • the PSS supernatant is washed away with water.
  • a solution of chitosan flu with a molecular weight> 300,000 g / mol in 0.5 mol / l NaCl is then added to the templates and adsorbed on the surface.
  • 7 layers of PSS and PAH are alternately applied with solutions of 1 g / 1 polymer in 0.5 mol / l salt. Wash 3 times with water between the coating steps.
  • a concentration of 2.3 g / l PSS-Rho was then determined inside the CS particles obtained in this way (FIG. 3a).
  • the concentration of PSS on the wall is particularly high, which is due to increased adsorption on the inner surface of the chitosan primer.
  • the silicate templates are extracted with 100 mL of a solution of 2 mol / l sodium fluoride in 1 mol / l acetate buffer pH 4. After 3 hours, the templates have completely dissolved and the capsules filled with PSS remain (FIG. 3b). A concentration of 1.8 g / l PSS-Rho was determined inside the capsules, which decreased slightly after storage for several weeks.
  • Figure 3 shows capsules made with negatively charged polymer inside; a) confocal image of CS particles filled with PSS-Rho, which are coated with chitosan (PSS / PAH) 3 PSS (rhodamine channel PMT2 800 V, image size 80 ⁇ m x 80 ⁇ m); b) Confocal image of capsules filled with PSS-Rho made of chitosan (PSS / PAH) PSS after removing the SiO 2 template (rhodamine channel PMT2 850 V, image size 80 ⁇ m x 80 ⁇ m).
  • PSS / PAH chitosan
  • TRITC-BSA 1 rhodamine labeled bovine serum albumin
  • BSA Bovine Serum Albumin
  • a solution of Chitosan-Flu with a molecular weight> 300,000 g / mol in 0.5 mol / l NaCl is then added to the templates and adsorbed on the surface.
  • 7 layers of PSS and PAH are alternately applied with solutions of 1 g / 1 polymer in 0.5 mol / l salt. Washes 3 times with water between the coating steps.
  • a concentration of 1.2 g / l BSA was determined inside the CS particles obtained (FIG. 4a).
  • the silicate templates were dissolved in 100 ml of a solution of 2 mol / l sodium fluoride in 1 mol / l acetate buffer at a pH of 5.
  • Figure 4 shows capsules made with protein inside; a) confocal image of CS particles filled with BSA-Rho (BSA marked with rhodamine) and coated with chitosan (PSS / PAH) 3 PSS (rhodamine channel PMT 850V, image size 80 ⁇ m x 80 ⁇ m); b) Confocal image of capsules filled with BSA-Rho Chitosan (PSS / PAH) 3 PSS after removing the SiO 2 template (rhodamine channel PMT 900 V, image size 80 ⁇ m x 80 ⁇ m).
  • BSA-Rho BSA marked with rhodamine
  • PSS / PAH chitosan
  • Sequential storage of 2 different active ingredients 10 mg of spherical, porous silica templates with a diameter of 10 ⁇ m and a pore size of 7 nm are suspended in 100 ⁇ L water (pH 6.5). 100 ⁇ L of a solution of 1 g / 1 of polyallylamine (PAH) labeled with rhodamine with a molecular weight of 70,000 g / mol are added and incubated for 12 h. The cationically charged PAH-Rho has accumulated inside the particles. There is no PAH in the supernatant.
  • PAH polyallylamine
  • a solution of 500 ⁇ L labeled chitosan with a molecular weight of 50,000-300,000 g / mol is added to the particles and incubated for a further 12 h.
  • a solution of chitosan with a molecular weight> 300,000 g / mol in 0.5 mol / l NaCl is added to the particles and adsorbed on the surface.
  • 7 layers of PSS and PAH are alternately applied with solutions of 1 g / 1 polymer in 0.5 mol / l salt. Washes 3 times with water between the coating steps. As the confocal images show (FIG.
  • the inside of the CS particles contains 2.5 g / 1 PAH-Rho and 7 g / 1 low-molecular chitosan flu.
  • the silicate templates were dissolved out with 100 mL of a solution of 2 mol / l sodium fluoride in 1 mol / l acetate buffer pH 4. After 3 hours the templates have completely dissolved and the capsules filled with PAH and chitosan remain (FIG. 5c, d). Concentrations of 1.7 g / 1 PAH-Rho and 7 g / 1 Chitosan-Flu were determined inside the capsules, which did not change after storage for several weeks.
  • FIG. 5 shows confocal images of CS particles and capsules, which are filled with 2 positively charged polymers PAH-Rho and low molecular weight chitosan-Flu and are encapsulated with chit (PSS / PAH) 3 PSS; a) CS particles in the rhodamine channel PMT2 600 V, image size 80 ⁇ m x 80 ⁇ m; b) CS particles in the fluorescein channel PMT1 500 V, image size 80 ⁇ m x 80 ⁇ m; c) Capsules in the PMT2 700 V rhodamine channel, image size 80 ⁇ m x 80 ⁇ m, d) Capsules in the PMT1 550 V fluorescein channel, image size 80 ⁇ m x 80 ⁇ m 5. Filling with nanoparticles
  • FIG. 6 a shows confocal images of capsules that are filled with positively charged magnetite nanoparticles and encapsulated with chit (PSS / PAH) 3 PSS (80 ⁇ m ⁇ 80 ⁇ m).
  • Figure 6b shows how the capsules can be collected in an Eppendorf tube using a magnet on the top.
  • Microcapsules with a solid structural framework inside 10 mg of spherical, porous silicate templates with a diameter of 10 ⁇ m and a pore size of 10 nm are suspended in 100 ⁇ L water (pH 6.5).
  • 100 ⁇ L of a solution of 1 g / 1 of polyallylamine (PAH) labeled with rhodamine with a molecular weight of 15,000 g / mol in 0.5 mol / l of NaCl are added and the mixture is incubated for 60 min with the temporary use of ultrasound.
  • PAH-Rho has accumulated inside the particles. The excess of PAH-Rho is washed away.
  • PAH-Rho is located inside the CS particle, while the Cy5-labeled PAH forms the shell.
  • the concentration was determined to be 21.5 g / 1 PAH-Rho.
  • the silicate templates were dissolved out with 100 L of a solution of 2 mol / l sodium fluoride in 1 mol / l acetate buffer pH 4. After 3 hours, the templates have completely dissolved and the capsules filled with the PSS / PAH-Rho remain (FIG. 7c). Concentrations of 16.9 g / 1 PAH-Rho were determined inside the capsules, which are guaranteed to be significantly higher due to the self-quenching occurring in the complex framework.
  • FIG. 7 shows confocal images of CS particles and capsules which are filled with a PAH-Rho / PSS complex and are coated with chit (PSS / PAH) 3 PSS a) CS particles in the rhodamine channel PMT2 600 V, image size 40 ⁇ m ⁇ 40 ⁇ m ; b) CS particles in the Cy5 channel PMT1 500 V, image size 40 ⁇ m x 40 ⁇ m; c) Capsule superimposed in the rhodamine and Cy5 channel, 2 holes were burned in the capsule with high laser power, which are location-stable, image size 40 ⁇ m x 40 ⁇ m, d) Capsules produced according to Example 1 (filled with PAH-Rho) after Drying, image size 40 ⁇ m x 40 ⁇ m e) Capsules with PAH-Rho / PSS framework after drying, image size 40 ⁇ m x 40 ⁇ m
  • FIG. 8 shows individual process steps for the production of microtemplates 16, which here consist of a filigree framework of polyelectrolyte and / or nanoparticle layers 14.
  • porous templates 2 are filled with alternately charged polyelectrolyte and / or nanoparticle layers 14, ie these materials coat the inner surface (pore surface) of template 2 and possibly also the outer surface of the template.
  • Microtemplate 16 back which can be surrounded by partially or largely closed polyelectrolyte and / or nanoparticle layers.
  • capsule shell 9 capsule shell 10
  • CS particles 12 13 microcapsule 14 polyelectrolytes / nanoparticles

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  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Medicinal Preparation (AREA)
  • Cosmetics (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)

Abstract

L'invention concerne un procédé pour produire des particules de type coeur-écorce (10) et des microcapsules (12). Ce procédé comprend les étapes suivantes: (A) au moins un principe actif (4) est adsorbé dans des matrices poreuses (2), ce qui permet d'obtenir des matrices (5) remplies de principes actifs; (B) les matrices (2) sont ensuite pourvues d'une couche de base (6), dans le but de faciliter la formation ultérieure de l'enveloppe (9) de la capsule; (C) l'enveloppe de la capsule est formée par application de couches de polyélectrolytes (8) chargés en alternance de manière positive et négative, ce qui permet d'obtenir des particules de type coeur-écorce chargées; (D) la matrice (2) est ensuite dissoute, ce qui provoque la libération des principes actifs (4) présents dans la matrice et leur passage à l'intérieur de la microcapsule; (E) les principes actifs (4) restent enfermés dans cette dernière ou sont libérés lentement de la capsule.
PCT/EP2005/002810 2004-03-19 2005-03-16 Procede pour produire des particules de type coeur-ecorce et des microcapsules au moyen de matrices microporeuses, particules de type coeur-ecorce et microcapsules, et leur utilisation Ceased WO2005089727A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP05716128A EP1729745B1 (fr) 2004-03-19 2005-03-16 Procede pour produire des particules de type coeur-ecorce et des microcapsules au moyen de matrices microporeuses, particules de type coeur-ecorce et microcapsules, et leur utilisation
CA002559477A CA2559477A1 (en) 2004-03-19 2005-03-16 Process for the production of cs particles and microcapsules using porous templates, cs particles and microcapsules, and use thereof
JP2007503286A JP2007529303A (ja) 2004-03-19 2005-03-16 多孔質テンプレートを用いたｃｓ粒子およびマイクロカプセルの製造方法、ｃｓ粒子およびマイクロカプセル、およびそれらの使用
US10/593,353 US7939103B2 (en) 2004-03-19 2005-03-16 Method for producing core-shell (CS) particles and microcapsules using porous templates, CS particles and microcapsules, and the use thereof

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Application Number Priority Date Filing Date Title
DE102004013637A DE102004013637A1 (de) 2004-03-19 2004-03-19 Verfahren zur Herstellung von CS-Partikeln und Mikrokapseln unter Verwendung poröser Template sowie CS-Partikel und Mikrokapseln
DE102004013637.8 2004-03-19

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EP (1) EP1729745B1 (fr)
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DE102004013637A1 (de) 2005-10-13
US20080020051A1 (en) 2008-01-24
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CA2559477A1 (en) 2005-09-29
EP1729745A1 (fr) 2006-12-13
JP2007529303A (ja) 2007-10-25

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